Lime-based sorbent for use in a flue gas treatment installation and process of manufacturing said lime-based sorbent

Patent metadata

Field	Value
Publication number	US-12440820-B2
Application number	US-202017760522-A
Country	US
Kind code	B2
Filing date	Sep 22, 2020
Priority date	Sep 23, 2019
Publication date	Oct 14, 2025
Grant date	Oct 14, 2025

Abstract

Lime-based sorbent suitable for use in a flue gas treatment process comprising at least 70 wt. % of Ca(OH) 2 and at least 0.2 wt. % to at most 10 wt. % of a first additive selected among the group of hydrogels of natural or synthetic origin, in particular superabsorbent polymers (SAPs) or in the group of cellulose ethers or a combination thereof, premix for use in a manufacturing process of said sorbent, process for manufacturing the sorbent and use of said sorbent in a flue gas treatment process.

First claim

The invention claimed is:

1. A lime-based sorbent in powder form suitable for a circulating dry scrubber process and for numerous passing cycles through a CDS facility comprising:
at least 70 wt. % of Ca(OH) 2 with respect to the total weight of said lime-based sorbent under a dry form after drying until constant weight at 150° C.,
at least 0.2 wt. % to at most 10 wt. % with respect to the total weight of said lime-based sorbent under a dry form after drying until constant weight at 150° C., of a first additive selected from the group consisting of hydrogels forming materials of natural or synthetic origin, superabsorbent polymers (SAPS) or cellulose ethers or a combination thereof,
having a BET specific surface area comprised of at least 3 m 2 /g, measured by manometry with adsorption of nitrogen after degassing in vacuum at 190° C. for at least 2 hours and calculated according to the multipoint BET method as described in the ISO 9277/2010E standard, and
having a total BJH pore volume of at least 0.01 cm 3 /g, determined by manometry with adsorption of nitrogen after degassing in vacuum at 190° C. for at least 2 hours and calculated according to the multipoint BJH method as described in the ISO 9277/2010E standard.

2. The lime-based sorbent according to claim 1 , wherein said first additive is selected from the group consisting of:
the group of hydrogels forming materials of synthetic origin including polyacrylates, polyacrylic acids, crosslinked polyacrylates and polyacrylic acids, or crosslinked acrylamide and acrylate copolymers partially neutralized with sodium and/or potassium, or
the group of hydrogels forming materials of natural origin including guar gum, alginates, dextran or xanthane gum or a combination thereof and/or;
the group of cellulose ethers, including hydroxyalkyl or carboxyalkyl cellulose ethers, carboxymethyl cellulose or hydroxyethyl methyl cellulose (HEMC).

3. The lime-based sorbent according to claim 1 , wherein said superabsorbent polymer is selected from the group consisting of crosslinked polymers of acrylic or methacrylic acid, crosslinked graft copolymers of the polysaccharide/acrylic or methacrylic acid, crosslinked terpolymers of acrylic acid or methacrylic acid/acrylamide/sulfonated acrylamide and their alkaline earth or alkaline metal salts.

4. The lime-based sorbent according to claim 1 , further comprising sodium wherein the amount of sodium expressed under its equivalent Na 2 O oxide form in said lime-based sorbent measured by XRF is of at least 0.1 weight % of sodium with respect to the total weight of said lime-based sorbent under a dry form.

5. A method of use in a flue gas treatment process, comprising contacting the flue gas with the lime-based sorbent according to claim 1 in a circulating dry scrubber process or dry sorbent injection process.

6. A flue gas treatment process wherein gas containing pollutants are circulated through a duct before reaching a particulate control device, comprising a step of injection of the lime-based sorbent according to claim 1 .

7. A process of manufacturing the lime-based sorbent according to claim 1 , the process comprising:
slaking quicklime with water in a hydrator via a non-wet route,
collecting a slaked lime at an exit of the hydrator, and
adding at least a first additive selected from the group consisting of hydrogels forming materials of natural or synthetic origin, superabsorbent polymers (SAPs) or cellulose ethers or a combination thereof;
wherein said first additive is added before, during or after said slaking, at a weight ratio relative to the weight of said slaked lime comprised between 0.2 and 10%, and wherein the amount of said slaked lime is expressed under equivalent CaO and the amount of said first additive is expressed under dry equivalent form after drying until constant weight at 150° C.

8. The process of manufacturing according to claim 7 , wherein the said first additive is selected from the group consisting of:
the group of hydrogels forming materials of synthetic origin including crosslinked polyacrylates or crosslinked acrylamide and acrylate copolymers partially neutralized with sodium and/or potassium,
the group of hydrogels forming materials of natural origin including guar gum, alginates, dextran or xanthan gum or a combination thereof or
the group of cellulose ethers, including hydroxyalkyl or carboxyalkyl cellulose ethers carboxymethyl cellulose or hydroxyethyl methyl cellulose (HEMC).

9. The process of manufacturing according to claim 7 , wherein
said first additive is provided at least partially in a solution or in a suspension and added to said water and/or to said slaked lime, and/or;
said first additive is provided at least partially under solid form and added to said quicklime and/or to said slaked lime.

10. The process of manufacturing according to claim 7 , further comprising a step of addition of a second additive, wherein said second additive is a salt or hydroxide of an alkali metal, before and/or during and/or after said slaking, wherein a content of said alkali metal is equal to or greater than 0.2% and equal to or less than 3.5% by weight with respect to the total weight of said slaked lime.

11. The process of manufacturing according to claim 7 , wherein a residence time of quicklime slaked inside the hydrator is between 5 and 45 minutes.

12. The process of manufacturing according to claim 7 , wherein said first additive is added before or during said slaking further comprising a step of drying said lime-based sorbent and/or a step of granulometric cutting of said lime-based sorbent and/or grinding or milling said lime-based sorbent.

13. The process of manufacturing according to claim 7 , wherein said first additive is added to said slaked lime after said slaking, the process further comprising:
a step granulometric cutting of said slaked lime;
a step of granulometric cutting of said first additive under a powdered form, and
a step of blending said slaked lime and said first additive in a homogenizing device.

Assignees

• Lhoist Rech Et Developpement Sa
• S A Lhoist Rech Et Developpment

Inventors

• Ligner Emanuelle
• Chopin Thierry
• Lorgouilloux Marion

Classifications

• B01J2220/68

  Superabsorbents · CPC title

• B01J2220/46

  Materials comprising a mixture of inorganic and organic materials (materials coated or impregnated on a carrier B01J20/32) · CPC title

• B01J20/3085

  Chemical treatments not covered by groups B01J20/3007 - B01J20/3078 · CPC title

• B01J20/3021

  Milling, crushing or grinding · CPC title

• B01J20/28059

  being less than 100 m2/g · CPC title